US9127097B2ActiveUtilityA1
P-N-P ligand
Est. expiryJan 25, 2032(~5.6 yrs left)· nominal 20-yr term from priority
C07C 2531/14C07C 2531/34C08F 4/69B01J 2531/62B01J 2231/20C07F 9/4883C07C 2531/24C08F 10/02B01J 31/187C07F 9/5325C07C 2/36
88
PatentIndex Score
2
Cited by
22
References
5
Claims
Abstract
A new P-N-P ligand is useful in ethylene oligomerizations. In combination with i) a source of chromium; and ii) an activator such as methylalumoxane; the ligand of this invention may be used to prepare an oligomer product that contains a mixture of high purity alpha olefins. In a preferred embodiment, the ligand of this invention enables a selective oligomerization in which the majority of the liquid product is a mixture of hexene and octene. The amount of by-product polymer that is produced in preferred oligomerization reactions is advantageously low.
Claims
exact text as granted — not AI-modifiedThe invention claimed is:
1. A process for the oligomerization of ethylene, wherein said process comprises contacting ethylene under oligomerization conditions with a catalyst system comprising
i) a source of chromium;
ii) a ligand defined by the formula
wherein Ar 1 is selected from the group consisting of aromatic hydrocarbyl and aromatic heterohydrocarbyl; Ar F is an aromatic fluorocarbyl oxide; Ar 3 and Ar 4 are independently selected from the group consisting of aromatic hydrocarbyl, aromatic heterohydrocarbyl and aromatic fluorocarbyl oxide; and R 1 is selected from the group consisting of hydrocarbyl and heterohydrocarbyl; and
iii) an activator.
2. The process of claim 1 when undertaken at a temperature of from about 10° C. to about 300° C. and a pressure of from about 5 atmospheres to about 150 atmospheres.
3. The process of claim 1 wherein said source of Cr is selected from the group consisting of chromium chlorides, chromium carbonyl, chromium carboxylates and chromium acetylacetonate.
4. The process of claim 1 wherein said activator comprises methylaluminoxane.
5. The process of claim 1 which is further characterized by producing a liquid product stream which contains greater than about 25 weight % octene-1.Cited by (0)
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